SE529270C2 - Procedure for boosting a Fischer-Tropsch diesel fuel where the fuel passes through a heated fuel filter - Google Patents

Abstract

Embodiments of the present invention are directed toward systems and methods of providing a low-emissions diesel fuel for use in cold climates. Such fuels may be prepared by a Fischer-Tropsch process and include a pour point depressant. Furthermore, the fuel is used in conjunction with a heated fuel delivery system so that low cloud points are not necessary. Fuels prepared according to embodiments of the present invention may be produced in higher yields than otherwise possible because a higher paraffin wax content can be tolerated, thus obviating the need to remove or exclude the wax. These fuels are characterized by a sulfur content less than 1 ppm, a cetane number greater than 60, an aromatics content less than 1 wt %, and a difference between the cloud and pour points that is greater than about 5° C. The present fuel may be prepared by a Fischer-Tropsch synthesis from any number of carbon-containing sources such natural gas, coal, petroleum products, and combinations thereof.

Description

20 25 30 35 (529 27ø 2 has been reached. The pour point can also be a rough indicator of the temperature at which the fuel will solidify in the fuel tank. Either of these two situations can be difficult, if not catastrophic, because an interruption in the fuel supply to an active engine will cause it to stop working.

Cloud point and pour point values can be viewed simultaneously to indicate a type of cold climate specification. Typically, the difference between the cloud point and the pour point is less than about 5 ° C where the cloud point is the higher of the two temperatures. While some fuel systems become clogged at the cloud point temperature, others may operate several degrees below the cloud point before plugging weakens the system. This is because low temperature filterability depends on the size and shape of wax crystals suspended in the fuel and not just whether or not they are present.

Another challenge to face in cold geographical locations is to get the engine to start in the first stage. When attempting to start a cold engine, the heat of the compression of the fuel in the combustion chamber is the only source of energy available to heat the fuel to a temperature where it can spontaneously ignite (approximately 750 ° F). Initially, the walls of the combustion chamber act as a heat sink instead of a heat source because they are located in a cold ambient instead of a warm operating temperature. Furthermore, since the cranking speed of the engine is less than the operating speed, the compression of the fuel is initially slow, which allows more time for the fuel to lose heat to the chamber walls.

The ability to start a cold engine depends on the cetane number of the fuel, which is a measure of the tendency of the fuel to burn spontaneously. In the cetane number scale, high values represent fuels that catch fire easily, and thus fuels with high cetane numbers perform better in diesel engines. Typically, a minimum cetane number of 40 is required to ensure adequate cold-start behavior, although higher numbers are desirable. When ambient temperatures are below freezing, starting aids may be necessary regardless of the cetane number of the fuel.

In addition to concerns about diesel fuel properties' in cold climate situations, there are growing concerns about excessive emissions from diesel engines. Emissions from diesel engines can be reduced if the sulfur content of the fuel is reduced to a level of approximately one part per million (ppm).

Emissions can also be reduced if the content of aromatic components of the fuel is less than about one percent by weight.

One of the techniques available to provide low-emission fuels is to produce them from products of a Fischer-Tropsch process. A Fischer-Tropsch synthesis is a process in which a starting material called synthesis gas (or "syngas"), which comprises carbon monoxide and hydrogen, is converted to a mixture of long chain hydrocarbons comprising olefins, paraffins and alcohols. The reaction can be considered as a hydrogenating oligomerization of carbon monoxide in the presence of a heterogeneous catalyst, and the reactions have been described by S. Mater and Lewis Hatch in Chemistry of Petrochemical Processes, 2nd Edition (Gulf Professional Publishing, Boston, 2001), pp. 121-126. »In the Fischer-Tropsch process provides a product which has a low content both in terms of sulfur and aromatic compounds. Thus, from the point of view of emissions, the products of the Fischer-Tropsch process are ideal. Unfortunately, fuels derived from this source also contain normal paraffins in the form of waxes in the diesel boiling range that solidify at cold temperatures.

To optimize a Fischer-Tropsch fuel for use in cold climates. it may be necessary to remove most if not all of the paraffins, especially those with the highest boiling point. Normal paraffins are typically treated in an isomerization process that transfers them to branched paraffins. However, this transfer is not completely selective and some of the normal paraffins are transferred to light by-products which cannot be blended into the diesel product without jeopardizing the safety of the fuel by simultaneously lowering the ignition temperature of the fuel. An alternative solution is to reduce the end point of the diesel fuel, which excludes normal paraffins with a high boiling point by "terminating" the distillation before they have a chance to distill over to the product. However, end point lowering and transfer techniques to reduce the wax content are not always desirable as solutions to the wax problem as each of these techniques reduces the yield of the product and hydrocarbon sources are in short supply.

What is needed is a diesel fuel designed for use in cold geographical locations and cold climatic conditions that can possibly be used in hot weather as well. Such a fuel will have a low sulfur content and low content of aromatic compounds to reduce emissions, and a high cetane number for combustibility. The technology lacks a fuel for cold climates whose paraffin wax content can be tolerated so that the fuel can be produced in higher yields than would otherwise have been possible.

SUMMARY OF THE INVENTION A present approach to making low emission fuels suitable for use in cold climates is to hydrate the petroleum feed under conditions which are so severe that the yield of the product is substantially reduced. Such a hydrotreating process is necessary to remove sulfur and aromatic compounds from the fuel, and to increase its cetane number. Another practice that contributes to lower yields involves lowering the distillation point so that higher molecular weight wax components cannot boil into the product-I stream, and thus these wax components are excluded from the final product.

The cloud point of the fuel will be higher if these paraffin waxes were distilled into the product.

Applicants are unaware of any reference which teaches these elements in combination: a diesel fuel derived from a low sulfur Fischer-Tropsch process, low content of aromatic compounds, and high cetane number ; substantially no plugging of fuel filter, substantially no solidification in the fuel tank; and higher production yields than conventional procedures. Conventionally, for use in cold climates, Fischer-Tropsch-derived diesel fuels are largely isomerized or the endpoints are reduced to low values. This reduces the yield.

Another parameter related to emissions from diesel engines is the cetane number, which describes the ability of a fuel to ignite spontaneously. Normal paraffins have high cell numbers that increase with molecular weight. Isoparaffins have a wide range of cetane numbers ranging from about 10 to 80. Molecules with many short side chains have low cetane numbers, while those with a side chain of four or more carbons have high cetane numbers. In general, it is desirable for the cetane number to be greater than or equal to about 60, but most preferably it may be greater than about 65 or even greater. 70. In accordance with one embodiment of the present invention, there is provided a Fischer-Tropsch-derived diesel fuel, the fuel comprising a sulfur content of less than about 1 ppm; a cetane number greater than about 60; a content of aromatic compounds which is less than about 1% by weight; and a pour point depressant.

Another embodiment of the present invention is directed to a method of amplifying a Fischer-Tropsch-derived diesel fuel, the method comprising adding a pour point depressant in an amount such that the difference between cloud point and pour point of the fuel is greater than about 5 ° C when the pour point is below about 0 ° C; and wherein the method comprises passing the diesel fuel through a heated fuel filter when the difference between the ambient temperature and the cloud point of the fuel is less than about 2 ° C so that filter re-plugging is substantially avoided. In the latter embodiment, the difference between the ambient temperature and the cloud point of the fuel is less than about 5 ° C.

BRIEF DESCRIPTION OF THE RELEASES Fig. 1A is a graphical illustration of the difference between cloud point and pour point of a conventional fuel used in a hot climate; Fig. 1B is a graphical illustration of the difference between cloud point and pour point of a conventional fuel used in a cold climate; and Fig. 1C is a graphical illustration of the difference between cloud point and pour point of an exemplary fuel of the present invention used in a cold climate.

DETAILED DESCRIPTION OF THE INVENTION In accordance with embodiments of the present invention, new methods are provided for providing a low emission diesel fuel for use in cold climates, wherein the fuel is synthesized by a Fischer-Tropsch process and the fuel has included in it a pour point depressant. In addition, the fuel can be transported through a fuel supply system which is either insulated and / or has at least a part of this system heated in it.

Part of the supply system that may be heated is the fuel filter. When an engine is equipped with a heated fuel filter, there is no longer a need to provide fuels with reduced cloud points. Thus, it is possible to produce fuels in higher yields than would previously have been possible since paraffin waxes do not need to be removed. However, when a pour point depressant is included in the composition, potential problems with fuel stagnation in the fuel tank are alleviated and such fuel flows freely in the fuel supply system even in cold weather. In a Fischer-Tropsch-derived diesel fuel of the present invention, it is characterized by: b a sulfur content of less than about 1 ppm; c a content of aromatic compounds of less than about 1% by weight; d a cetane number greater than about 60; and e a difference between cloud point and pour point greater than about 5 ° C.

Embodiments of the present invention include the use of heated fuel filters, the use of pour point depressants, and the production of diesel fuels from a Fischer-Tropsch process. Each of these embodiments is known separately in the art, but not in combination. The cloud point and pour point of a fuel will be defined in more detail briefly, at present it is sufficient to say that the cloud point is higher than the pour point and that a cloud point / pour point difference greater than 5 ° C is an indication of 1) that paraffin waxes has not been removed (or completely removed) from the fuel and 2) that the fuel contains a pour point depressant.

The objects of the present embodiments include fuel production in high yields, low emissions during fuel combustion, easy engine starting, and ability of the engine to tolerate a paraffin wax content in the fuel when the fuel is used in cold climates. Preferably, the fuel ignites easily in cold temperatures. Diesel fuels and fuel supply systems using the present fuel have the ability to tolerate a certain content of paraffin wax in cold climates, and this allows the fuel to be produced in higher yields than would otherwise have been possible. Figs. 1A-C illustrate differences between cloud point and 'pour point' of different fuels used in hot and cold climates, where the comparison is made in relation to an arbitrary temperature scale shown generally at reference number 10. The temperature increases with the height of the graph. In Fig. 1A, a conventional fuel is used in a warm climate. The difference between cloud point 11A and pour point 12A is plotted by reference number 13A and this difference is approximately 5 ° C for a conventional fuel. Also shown in Fig. 1A is an ambient temperature 14A which is high due to the hot climate and a filter temperature 15A which is also high due to the warm ambient temperature.

Fig. 1B illustrates analog temperature levels for a conventional fuel used in a cold climate. For this situation, the cloud point 11B and the pour point 12B are each lower than in the previous case because paraffin waxes have been removed from the fuel either by isomerization of normal long chain paraffins, or by reducing the boiling range of the fuel. Since the cloud point 11B and the flow point 12B are reduced by approximately the same amount from their levels in Fig. 1A, the temperature difference 138 is still about 5 ° C. As would be expected for this cold climate situation, the ambient temperature 14B and the filter temperature 15B are lower than in the warm climate of Fig. 1A and the filter temperature 15B is approximately the same as the ambient temperature 14B since there is no filter heater.

Fig. 1C illustrates the situation of an exemplary fuel according to the present invention used in a cold climate. The ambient temperature 14C is at about the same level as 14B because the fuel is also used in a cold climate. In the case of the fuel of the present invention, none of the paraffin wax content has been removed and therefore the cloud point 11C is higher than the cloud point 11B. The cloud point 11C can be either higher or lower than the cloud point 11A.

Referring again to Fig. 1C, the pour point 12C is lower than the pour point 12A since the fuel of the present invention contains a pour point depressant and the conventional fuel in Fig. 1A does not. The pour point 12C may be either higher or lower than the pour point 12B, but since the effect of isomerizing paraffin wax or reducing the distillation end point may be greater in reducing the surface point than the reduction caused by a pour point depressant, the pour point 12B is often lower than 12C In any case, the difference 13C between the cloud point 11C and the pour point 12C is greater than 5 ° C and this is indicative of a fuel composition according to the present invention.

Normally, a fuel with a high cloud point would not be suitable for cold climate situations because the wax content of the high cloud point fuel has the potential to plug the fuel filter, but the use of a fuel filter heater according to embodiments of the present invention ensures that the filter temperature 15C is higher than the cloud point. and thus the paraffin waxes in solution remain empty a cold climate. In one embodiment, the difference 13C is greater than about 5 ° C. In another embodiment of the present invention, the difference 13C is greater than about 10 ° C. In yet another embodiment, the difference 13C is greater than about 15 ° C.

Cold Climate Specifications Diesel fuel specifications are generally addressed through ASTM D-975, Standard Specification for Diesel Fuel Oils. This specification sets limits or requirements for the value of certain properties, which include ignition temperature, viscosity, sulfur content, cetane number and aromaticity, but D-975 does not specifically address situations in cold climate. The specifications relevant for low temperature diesel fuel for use in the United States are described in ASTM D-985. This specification describes how the temperature and thus the acceptable cloud point varies with month and place in the United States.

Suitable values for these properties of diesel fuels for use in countries other than the United States are similarly described in CONCAWE reports “Motor vehicle Emission Regulations and Fuel Specifications.” Despite the location, cold climate characteristics should be considered in relation to typical ambient temperatures for this region.

Details regarding four tests used in industry to quantify low-temperature properties will now be presented. These properties are cloud point and float point. already alluded to and cold filter re-plugging point (CFPP) and low temperature flow test (LTFT) not yet mentioned. In some cases, CFPP can be approximated by the cloud point. Further details on cetane number will also be provided.

Cloud point and pour point have been precisely defined by J.G. Speight in Handbook of Petroleum Analysis (Wiley-lnterscience, New York, 2001) page 459. Speight defines the cloud point as the temperature at which paraffin wax or other solids begin to crystallize or separate from solution, giving rise to a cloudy behavior. in the oil when the oil is cooled under prescribed conditions. Pour point has been defined as the lowest temperature at which oil will flow or flow when cooled without disturbance under fixed conditions. Cloud point is relevant for steady and uninterrupted flow of fuel through a fuel supply system. Pour point is relevant for solidification of diesel in fuel tank.

Measurement of cloud point and pour point has been discussed by Speight on pages 144-145 in the above reference. In accordance with these methods, oil is charged into a glass test tube equipped with a thermometer, and the test tube is then immersed in one of three baths containing coolant.

The sample is dried and filtered at a temperature of 25 ° C higher than the expected cloud point. It is then placed in a test tube and progressively cooled. The sample is inspected for milkiness at a temperature range of 1 ° C. See ASTM D-97, ASTM D-5327, ASTM D-5853, ASTM D-5949, ASTM D-5950, ASTM D-5985, IP 15, lP 219 and lP 441.

The pour point of petroleum is determined using a similar technique, and it is the lowest temperature at which the oil flows. It is in fact 1 ° C above the temperature at which oil ceases to flow. To determine the pour point, the sample is first heated to 46 ° C and cooled in air to 32 ° C before the test tube is immersed in the same series of coolants as used to determine the cloud point. The sample is inspected at a temperature range of 2 ° C by retracting the test tube and holding it in a horizontal position for 5 seconds. No flow of oil in the test tube should be observed during the time interval. See ASTM D-97 and IP 15. 10 15 20 25 30 35 '529 270 8 A dynamic test that has become widely accepted in Europe is the cold filter re-plugging point of distillate fuels (CFPP). In this test, the sample is cooled by immersion in a constant temperature bath. Thus, the cooling rate is non-linear but fairly fast, about 40 ° C per hour. CFPP is the temperature of the sample with 20 ml of the fuel that first fails to pass through a wire mesh for less than 60 seconds. CFPP seems to overestimate the benefit of using certain additives, especially for North American vehicles.

A similar dynamic test developed in the United States is the Low Temperature Flow Test (LTFT). In contrast to CFPP, LTFT uses a slow constant cooling rate of 1 ° C per hour. This speed was chosen to resemble the temperature behavior of the fuel in the tank of diesel truck left overnight in cold environment with its engine turned off. LTFT has been found to correlate well with low temperature function field tests. The cetane number of a diesel fuel measures up to the tendency of the fuel to ignite spontaneously. ASTM D 613 is the standard test method for determining the Cetane number of a diesel fuel oil. In the cetane scale, high values represent fuels that ignite easily, and therefore perform better in a diesel engine. Two specific hydrocarbons define the cetane number scale: 2,2,4,4,6,8,8-heptamethylnonane (also called isocetane), which has a cetane number of 15 and n-hexadecane (cetane) which is assigned a cetane number of 100. These hydrocarbons are primary reference fuels for the method. Originally, the cetane number of a fuel was defined as the volume percentage of n-hexadecane (zero cetane number) in a mixture of n-hexadecane-1-methylnaphthalene which gives the same ignition delay as the test sample, but when the low reference fuel changed an equation to pour the cetane number scale consistently with standards of origin.

Diesel Fuel Emissions Emissions from a diesel engine generally include hydrocarbons, carbon monoxide, nitrogen oxides (NOX), particulate solids (PM), and sulfur oxides (SOX). When hydrocarbon fuel is combusted with the correct amount of air in a diesel engine, the exhaust gases produced mainly include water vapor, carbon dioxide and nitrogen gas. Deviations from this ideal combustion lead to the production of volatile organic compounds (VOCs), as well as emissions listed above. Diesel engines are significant emitters of particulate matter and oxides of nitrogen, and emit carbon monoxide and volatile organic compounds to a lesser extent.

The sulfur content of diesel fuel affects emissions in particulate form because some of the sulfur in the fuel is transferred to sulphate particles in the exhaust gases. The fraction transferred to particulate matter varies from engine to engine, but there is generally a linear decrease in particulate matter as sulfur is reduced. For this reason, the Environmental Protection Agency (EPA) limits the sulfur content of road diesel fuel (so-called "low sulfur diesel fuel") to 0.05% by weight maximum, while some states as California applies this level to all vehicle diesel fuels, both on and off roads.

The cetane number still has an effect on emissions. By increasing the cetane number, fuel combustion increases and tends to reduce NO and particulate emissions. NO, seems to be reduced in most engines, while reduction of particulate emissions is more due to the engine and does not seem to occur universally. The effect of increasing the cetane number on the reduction of these emissions can be non-linear in such a way that the effect is most noticeable at low cetane numbers.

By reducing the content of aromatic compounds in the diesel fuel, NOX and particulate emissions in certain engines are also reduced. Polynuclear aromatic compounds appear to be more critical for this effect than single ring aromatic compounds.

Fischer-Tropsch Process The Fischer-Tropsch process was adapted as a means of converting natural gas to liquid fuels, but Fischer-Tropsch-derived fuels can be prepared from any amount of carbonaceous sources which include natural gas, coal, petroleum products and combinations thereof. For this reason, the process is also known as a 'gas-to-liquid' transmission. In a modern implementation of the Fischer-Tropsch process, natural gas, mostly methane, is reacted with air over a first catalyst to create synthesis gas, which is a mixture of carbon monoxide and hydrogen gas. This gas mixture, also known as "syngas", is then converted to liquid hydrocarbons using a diesel boiling point using a second catalyst.The material prepared from this process has many advantageous attributes, which include high cetane number and essentially no sulfur or aromatic content.

The Fischer-Tropsch process provides a product which is lower in sulfur and aromatic content, with a sulfur content approximately typically below 1 ppm (parts per million) and the aromatic content approximately below 1% by weight. The products of a Fischer-Tropsch process are typically hydrogenated to remove traces of olefins and oxygenates, and this results in a product that contains mostly paraffins. Usually the product contains more than about 90% by weight of paraffins, but may contain more than 95% by weight and up to more than about 98% by weight of paraffins.

Unfortunately, a type of normal paraffin is a wax in the diesel boiling range that can be present as a solid at cold temperatures. The normal paraffins with the highest boiling point have the highest melting points. Thus, it may be advantageous to remove most if not all of the normal paraffins, especially those with the highest boiling point, to use the fuel in cold climates, but this reduces the production yield.

Normal paraffins are typically removed by an isomerization process which transfers them to isoparaffins. However, the transfer is not 100% selective, and during the isomerization process, some of the normal paraffins can be transferred to light by-products which are not blended into a diesel fuel product while maintaining a safe ignition temperature. .

Alternatively, the distillation end point of the diesel fuel can be reduced. Catalysts and conditions for carrying out Fischer-Tropsch synthesis are well known to those skilled in the art and are described e.g. in EP 0 921 184 A1, the content of said document being in its entirety. In the Fischer-Tropsch synthesis process, liquid and gaseous hydrocarbons are formed by touching a synthesis gas (syngas) comprising a mixture of H 2 and CO with a Fischer-Tropsch- incorporated by reference in catalyst under suitable temperature and pressure reactive conditions. The Fischer-Tropsch reaction is typically carried out at temperatures from about 300 to 700 ° F (149 to 371 ° C). preferably from about 400 to 550 ° F (204 to 228 ° C); pressures of about 10 to 600 psia (0.7 to 41 bar), preferably 30 to 300 psia (2 to 21 bar) and catalyst space velocities of about 100 to 10,000 cc / g / hr, preferably 300 to 3000 cc / g / hr hr. The products of a Fischer-Tropsch process can range from G1 to Czoot, with a majority of the products in the Cs-Cioof range.

A Fischer-Tropsch synthesis reaction can be performed in a variety of reactor types which includes e.g. fixed bed reactors containing one or more catalyst beds, slurry reactors, fluidized bed reactors or a combination of different types of reactors. Such reaction processes and reactors are well known and documented in the literature. A preferred process in accordance with embodiments of the present invention is the slurry Fischer-Tropsch process, which uses superior heat and mass transfer techniques to remove heat from the reactor, since the Fischer-Tropsch reaction is strongly exothermic. In this way it is possible to produce paraffin hydrocarbons with a relatively high molecular weight.

In a slurry process, a syngas comprising a mixture of H 2 and CO is bubbled up as a third phase through a slurry formed by dispersing and suspending a particulate Fischer-Tropsch catalyst in a liquid comprising hydrocarbon products from the synthesis reaction. Accordingly, the hydrocarbon products are at least partially in liquid form under the reaction conditions. The molar ratio of hydrogen to carbon monoxide can range widely from about 0.5 to 4, but is more typically in the range of about 0.7 to 2.75, and preferably from about 0.7 to 2.5. An especially preferred Fischer-Tropsch method is taught in EP 0 609 079, which is also fully incorporated herein by reference.

Suitable Fischer-Tropsch catalysts include one or more groups of VIII catalytic metals such as Fe, Ni, Co, Ru and Re. In addition, a suitable catalyst may contain a promoter. Thus, a preferred Fischer-Tropsch catalyst comprises effective amounts of cobalt and one or more of the elements Re, Ru, Pt, Fe, Ni, Th, Zr, Hf, U, Mg and La on a suitable inorganic support material, preferably a material which comprises one or more of the refractory metal oxides. In general, the amount of cobalt present in the catalyst is between about 1 and about 50% by weight of the total catalyst composition. The catalysts may also contain basic oxide promoters such as ThO 2, LazO 3, IV 10 O 2 and TiO 2, promoters such as ZrO / ln, Ni and Re. Support materials including alumina, silica, magnesia and titania or mixtures thereof can also be used. Preferred support materials for cobalt-containing catalysts include titania.

Exemplary catalysts and their preparation can be found, among others, in U.S. Patent No. 4,568,663. As mentioned earlier, Fischer-Tropsch synthesis products include paraffin waxes.

The waxy reaction product includes hydrocarbons boiling above about 600 ° F, which in refinery terminology includes a vacuum gas oil fraction through heavy paraffins, with increasing minor amounts of material down to about C10. In one embodiment of the invention, the diesel fuel is formulated to comprise a 95% point as measured by ASTM D-2887 exceeding 625 ° F (329 ° C). In another embodiment of the invention, the fuel is formulated to comprise a 95% point as measured by ASTM D-2887 in excess of 650 ° F (343 ° C). In yet another embodiment of the invention, the fuel is formulated to comprise a 95% point as measured by ASTM D-2887 in excess of 690 ° F (366 ° C).

Pour point depressants Conventionally, two general approaches have been used to take care of low temperature function. A first approach is aimed at reducing the wax content of the fuel at refinery level and / or by treating the fuel with an additive that effectively removes the negative effects of the wax presence. For example. For example, diesel fuels can be produced from a crude oil precursor that inherently has a low content of paraffin wax. Similarly, fuel can be produced by refining crude oil to a lower endpoint, thus avoiding the inclusion of heavier, longer chain paraffin waxes. Alternatively, a first fuel with a high wax content can be mixed with a second fuel with a low wax content, thus diluting the concentration of wax in the mixture relative to the high level of the first fuel. Finally, a fuel with a high wax content can be treated with an additive that substantially prevents the waxes from precipitating out of solution at low temperatures. The first two approaches strive to avoid a high wax content from the beginning, while the latter two either reduce or prevent the effects of a high wax content. in Pour Point depressors are known in the art. These compounds are additives that lower the pour point of a diesel fuel, and thus improve its cold flow properties.

Chemically, they are polymers that interact with wax crystals before the waxes can precipitate out of solution. Pour point additives have a long, linear paraffinic component and a branched component. The linear component is incorporated within a particulate wax molecule, while the branched component prevents multiple wax molecules from agglomerating (thereby forming an interconnected structure throughout the hydrocarbon phase). It is the branched component of the pour point depressor that prevents a large wax crystal from solidifying / precipitating and thus the pour point temperature of the diesel fuel is lowered.

The polymer wax interactions are fairly specific, so a particular additive generally does not perform equally well in all fuels. Furthermore, in order to be effective, additives should be mixed into the fuel before any wax is formed; that is, when the fuel temperature is still above the cloud point.

There are several classes of branched components: fumarates based on alkylation of olefins with maleic anhydride followed by esterification of an alcohol; b branched alkyl aromatics (naphthalenes) based on alkylation of -AR-CH 2 -AR- functionalities with olefins and or alcohols; c acrylates based on alkylation with olefins and possibly alcohols; and d acetates based on the reaction of polymeric olefins with acetic acid.

An example of fumarate-based pour point depressants is described in U.S. Patent No. 4,240,916 which discloses an oil-soluble copolymer useful as a pour point depressant for lubricating oils and which consists of approximately uniform molar amounts of 1-olefins and maleic anhydride, the 1-olefins being present in a mixture comprising from about 25 to 75, preferably 30 to 55, mole percent of straight chain C20-C24 1-olefins and from about 25 to 75, preferably 45 to 70, mole percent of 010-014 1-olefins. These copolymers are oil-soluble, substantially free of olefin unsaturation and have a number molecular weight of from 1,000 to 30,000. The pour point depressant activity of these copolymers is enhanced by esterification with a C usable with Lubricant in an amount of from 0.01 to 3% by weight based on the total weight of the mixture.

As an example of alkyl aromatic pour point depressants, these are described in U.S. Patent Nos. 4,880,553 and 4,753,745. The compounds described in these patents may be represented by the general structural formula Ar (R) - [Ar '(R')] ,, - Ar ", where Ar, Ar 'and Ar each aromatic moiety is substituted with up to 3 substituents; (R) and (R ') represent alkylene group having about 1 to 100 carbon atoms provided that at least one of (R) and (R') is C1-1z, and n is 0 to about 1000; provided that if n is 0, then (R) is CH; and each aromatic moiety is independently substituted with 0 to 3 substituents having an aromatic moiety having at least one substituent, the substituents being selected from the group consisting of a substituent derived from an olefin and a substituent derived from a chlorinated hydrocarbon. The composition of the invention includes compounds ranging in molecular weight from about 271 to about 300,000. Examples of acrylate-based pour point depressants will now be discussed. U.S. Patent No. 6,172,015 discloses polar monomer-containing copolymers derived from at least one α-unsaturated carbonyl compound, such as alkyl acrylates and one or more olefins, such as olefins containing ethylene and C ) an average ethylene sequence length of from about 1.0 to less than about 3.0; . (b) an agent of at least 5 branches per 100 carbon atoms of copolymer chains comprising the copolymer; (c) at least about 50% of the branches are methyl and / or ethyl branches; (d) substantially all of the incorporated polar monomer present at the terminal position of the branches: (e) at least about 30% of the copolymer chains terminated with a vinyl or vinylene group; (f) a number average molecular weight, Mn, ranging from about 300 to about 15,000 when the copolymer is intended for dispersant or wax crystal modifier uses and up to about 500,000 when intended for viscosity modifier uses; and (g) substantial solubility in hydrocarbon and / or synthetic base oil. The copolymers are prepared using late transition metal catalyst systems and, as an olefin monomer source other than ethylene, preferably inexpensive, highly dilute refinery or steam cracker feed streams which have undergone only limited purification steps. Where functionalization and derivatization of these copolymers is necessary for such additives, this is simplified by olefinic structures available in the copolymer chains.

U.S. Patent No. 5,955,405 discloses non-dispersing polymethacrylate copolymers comprising from about 5 to 15% by weight of butyl methacrylate; from about 70% to about 90% by weight of a C 10 -C 15 alkyl (meth) acrylate; and from about 5 to about 10% by weight of a CMS-C 1-6 alkyl methacrylates to provide excellent low temperature properties of lubricating oils.

U.S. Patent No. 4,533,482 discloses hydrogenated diolefim lower alkyl acrylate or methacrylate copolymers and the use of these copolymers to improve the viscosity index (VI) of lubricating oils. The preferred copolymer is a fully hydrogenated, high molecular weight copolymer of 1,3-butadiene and methyl methacrylate containing at least about 71 mol / ° 1,3-butadiene. A pour point depressant incorporates a higher alkyl methacrylate into the copolymer and is prepared by graft polymerization of a polar nitrogen-containing graft monomer into the polymer.

U.S. Patent No. 4,359,325 discloses copolymers comprising acrylic esters, dicarboxylic compounds and diisobutylene functionalities. The number average molecular weight of these copolymers ranges from 500 to 250,000 are useful for improving the cold flow properties of lube oils and other hydrocarbon oils such as diesel oil, heavy fuel oils, excess fuel oil and crude petroleum. Physically, a fuel that has had a pour point depressant added (a so-called "added fuel") will exhibit a difference between the cloud point and the pour point of more than 5 ° C. Chemically, acrylic pour point depressants are perhaps the most commonly used in the art, and it is preferred in accordance with at least some of the embodiments of the present invention.

As shown in the examples below, pour point depressants are effective in reducing the pour point, but in general they are not particularly effective in reducing the cloud point (or the cold filter re-plugging point, which is related) when used in fuels at economic levels. Additional solutions to the problems presented by the cloud point are necessary, and these may include heating one or more of the various fuel supply system components. In accordance with one embodiment of the present invention, the difference between the cloud point and the pour point of the fuel is greater than about 10 ° C, but in another embodiment the difference is greater than about 15 ° C. In one embodiment of the present invention, the cloud point of the fuel is less than about 0 ° C, but it is less than about -15 ° C in another embodiment, and less than about -25 ° C in yet another embodiment. .

Heated fuel systems The second of the two general approaches used to take care of low temperature operation involves heating the fuel at a specific location within the fuel supply system. Factory facilities and vehicles may be equipped with fuel tank or fuel filter heaters, and / or insulation around fuel lines or other components of the fuel supply system. Fuel pumps, filters and other supply system components can be positioned adjacent to the engine to facilitate heat transfer from the engine. Another practice involves pumping more fuel to the injectors than the engine actually needs, so that excess fuel, which has now been heated by the engine, can be circulated back to the fuel tank.

Fuel filter heaters are known in the art. Desirable aspects of a heated fuel filter system in accordance with embodiments of the present invention are that: a the filter is heated to a temperature above the cloud point of the fuel; b the energy is supplied from a source within the vehicle, if it is a vehicle, but the energy source can be either internal or external in relation to the engine; and'c the fuel filter may be sealed to prevent leakage of fuel into the environment.

Preferably, the temperature of the filter is a sufficient amount above the cloud point of the fuel so that opportunities for wax plugging within the filter are substantially reduced. In accordance with one embodiment of the present invention, the temperature of the fuel filter is at least 5 ° C above the cloud point of the fuel, but in other embodiments the temperature of the fuel in the filter may be at least 10 ° C, or at least 15 ° C. higher than the cloud point.

The energy source providing heat to the fuel filter can originate from any number of locations, such as engine cooling systems, resistance heating sources including glow plugs, other electrical sources such as a battery, alternator or other onboard source, crankcase lubrication system, combinations of the above sources and the like. .

Heating of the filters can take place either in a continuous manner or in a periodic manner. In an exemplary embodiment, a sensor is used to detect increases in pressure drop across the filter, where a large pressure drop is experienced if solidified wax crystals should plug the filter, at which time the heater would be activated to drive the wax crystals back into solution. The sensor would operate in a negative feedback loop whereby the decrease in pressure decrease as a result of the wax dissolution would cause the heater to turn off until the next cycle. In this way, it is not necessary to operate the heating device continuously.

In another embodiment, multiple methods of providing heat can be used during different phases of engine use. For example. For example, the filter may be electrically heated during start-up, and then later heated by engine heat from the cooling system or lubricating oil as the engine reaches and maintains operating temperature.

Appropriate safety devices can be incorporated with these fuel filter heating systems to prevent overheating of the fuel supply system. Overheating a fuel system can create a potentially dangerous fire hazard. Such safety devices are known in the art and include self-regulating heat tapes, temperature detectors connected to shut-off devices and the like. Using heat from the cooling system or engine oil reduces the risk of overheating.

Various embodiments of the present invention are presented in the following examples.

Example 1 Preparation of a paraffinic Fischer-Tropsch diesel fuel A mixed high paraffinic feedstock with material boiling in the lighter half of the distillate fuel product, and material boiling over the end point of the product was prepared from three individual Fischer-Tropsch components. i 10 15 529 270 16 Table l Properties of highly paraffinic Fischer-Tropsch raw material components Properties Component 1 Component 2 Component 3% by weight in mixture 27.8 23.1 49.1 Gravates, ° Ai => 1 56.8 44.9 40-0 Sulfur, ppm <1 * <1 Oxygen, ppm by Neut. Act. 1.58 0.65 Chemical types,% by weight by GC-MS Paraffins 38.4 62.6 85.3 Olefins 49.5 28.2 1.5 Aikohøier, 11.5 7.3 9.3 Other species 0.5 3.9 3 »8 Distillation by D-2887, ° F with respect to weight% 0, 5/5 80/199 73/449 521/926 1 0/30 209/298 483/551 666/758 50 364 625 840 70/90 417/485 691/791 926/1039 96 / 99.5 518/709 872/1071 1095/1184 The mixture is prepared by continuously feeding the various components downstream of a hydroprocessing reactor. The reactor was filled with a catalyst containing alumina, silica, nickel and tungsten. The reactor was sulphinated before use. The LHSV was varied between 0.1 and 1.4 to investigate this effect, the pressure was constant at 1000 psig and the recovery gas velocity was 4000 SCFB. The transfer per pass was maintained at approximately 80% below the reuse cutpoint (665-710 ° F) by adjusting the catalyst temperature.

The product from the hydroprocessing reactor (after separation and recycling of unreacted hydrogen) was continuously distilled to provide a gaseous by-product, a light naphtha, diesel fuel and an unconverted fraction. The unconverted fraction was returned to the hydropressure reactor. The temperatures of the distillation column were adjusted to maintain the ignition temperature and the cloud point at their target values of 58 ° C for the ignition temperature and -18 ° C for the cloud point. 10 15 529 270 17 The yield of diesel fuel that could be produced from this raw material that met both the ignition and cloud point specifications was over 80 wt / °. The effect of LSHV on 0.7 increased the acceptable endpoint of the diesel fuel, which in turn increased the yield. It was obvious that operating at a low LHSV increased the isomerization of the heaviest portion of the diesel fuel which made it possible to increase the end point and in turn to increase the yield. Thus, it is preferred to operate this hydroprocessing unit at 1.5 LHSV or lower, preferably 1.0 LHSV or lower, and most preferably 0.75 LHSV or lower.

From this study, limits of 95% by weight / ° of diesel fuel can also be proposed. As noted earlier, it is desirable to maximize diesel yield, and incorporate as much heavy material as possible to achieve this goal. But the incorporation of heavy material is limited by the diesel cloud point. Incorporation of heavy materials increases the ability of the diesel fuel to incorporate light material near the ignition point, thus increasing the yield. Thus, the maximum diesel yield is obtained when the product is produced at or near the ignition and cloud point specifications, and with as sharp a distillation separation as possible. It is desirable to have 95% points as measured by ASTM D-2887 of a diesel fuel by this process exceeding 625 ° F, preferably exceeding 650 ° F and more preferably exceeding 690 ° F.

Diesel fuel was mixed resulting from several hours of consistent action at 1.4 LHSV to provide the representative product in Table ll:: 529 270 18 Table ll Properties of diesel fuel Gravity, ° API 52.7 Nitrogen, ppm 0.24 Sulfur, ppm <1 Water, ppm by Karl Fisher, ppm 21.5 Pour point, ° C Cloud point, ° C '15 Ignition temperature, ° C 58 Auto-ignition temperature, ° F 475 Viscosity at 2s ° C, cSt 2,564 / Viscosity at 40 ° C, Est 1/981 Cetane number 74 Aromatic compounds by supercritical fluid chromatography. weight-Wo <1 Neutralization number »0 Ash oxide, wick% <0.001 Ramsbottom carbon residue, weight% 0.02 Cu-strip corrosion 1A Color, ASTM D1500 0 GC-MS analysis Paraffins, weight ° / ° 100 Paraffin i / n ratio 2.1 Oxygen as oxygenates, ppm <6 Oils, weight-Wo '0 Average carbon number 14.4 Destination by D-2887 by weight-Wo, ° F and D-86 by volume-Vu, ° F 0-2887 D-86 0, 5/5 255/30 329135 0 6 10/20 326/36 366/39 8 3 30/40 406144 419/44 9 9 50 487 480 60/70 523/56 510/53 2 9 80/90 600/63 567 / 59 7 7 95/995 659/70 615/63 5 0 '10 15 20 25 i 529 270 f 19 In practice, the cloud point of the fuel can be adjusted by adjusting the end point of the fuel. Preferably the cloud point is less than 0 ° C, more preferably less than -15 ° C, and most preferably less than -25 ° C. While the use of the pour point depressor primarily affects the pour point, it will also have an effect, albeit less, on the cloud point. Thus, these cloud point levels are on the fuel before the addition of pour point depressors.

Example II Effect of pour point depressants The following two pour point depressants (PPDs) were mixed with diesel fuel in Example I: a. Plexol 156 (full name is Viscoplex 1-256), supplied by Rohm & Haas, a polyalkyl methacrylate diluted in a solvent which is neutral oil; and b. TDA 1197, supplied by Texaco Fuel Additives, an ethylene vinyl acetate copolymer in an aromatic solvent.

PPD Cloudburst Pour Point Difference Fuel Point âçimhng 'mg / kg Type ° C ° C ° C FT diesel fuel - _19 -24 5 FT diesel fuel + 1 Plexgl 156 -19 _24 5 FT diesel fuel + 4 Plexol 156 -20 -27 7 FT diesel fuel + 30 TDA 1197 -18 -24 6 FT diesel fuel + 100 TDA 1197 -18 -27 9 FT diesel fuel + 300 TDA 1197 -18 -36 '18 Both depressions reduced the pour point, but did not significantly reduce the cloud point. Thus, they can be used to reduce the pour point of a fuel with a high pour point, while relying on heated fuel filters to solve the problems associated with a high cloud point, as discussed earlier.

Unfortunately, analysis of the pour point depressants in fuel is difficult because they are high molecular weight components present in the fuel in relatively small amounts. The most effective method for determining the presence of a pour point depressant additive is to investigate the difference between cloud point and pour point. In the presence of the additive, the difference between cloud points and pour points increases from its typical value of less than about 5 ° C to a value of more than about 5 ° C. In other embodiments, the difference is more than about 10 ° C, and more preferably more than about 15 ° C. In order to be effective, a pour point depressant should be used in amounts greater than about 10 mg / kg. In some embodiments, the concentration of pour point depressant is used in an amount greater than about 50 mg / kg but less than about 1000 mg / kg. In still other embodiments, the pour point depressant is used in an amount greater than about 100 mg / kg but less than about 500 mg / kg. While the measurements of pour point depressants in fuel are difficult, they can be made by size exclusion chromatography (SEC), preferably when the separated fractions are analyzed by an evaporative light scattering detector. This technique can determine the presence and characteristics of high molecular weight additives in fuels at concentrations above about 10 ppm.

Many modifications of the exemplary embodiments of the invention described above will readily occur to those skilled in the art. Accordingly, the invention is to be understood as including all structure and methods falling within the scope of the appended claims.

Claims (20)

10 15 20 25 30 35 529 270 P1101287SEOO 21 Patent claims A method of amplifying a diesel fuel derived from a Fischer-Tropsch process wherein the fuel is formulated so as to comprise a 95% point as measured by ASTM D-2887 in excess of 329 ° C, the method comprising: a adding a pour point depressant in an amount such that the difference between the cloud point and the pour point of the fuel is greater than about 5 ° C when the pour point is below about 0 ° C; and b. passing the diesel fuel through a heated fuel filter when the difference between the ambient temperature and the cloud point of the fuel is less than about 2 ° C so that filter plugging is substantially avoided. The method of claim 1, wherein the difference between the ambient temperature and the cloud point of the fuel is less than about 5 ° C. The method of claim 1 wherein the fuel comprises: a. A cetane number greater than about 60; and b. a pour point depressant; wherein the difference between the cloud point and the fl surface point of the fuel is greater than approximately 5 ° C. The method of claim 3 wherein the difference between the cloud point and the pour point of the fuel is greater than about 10 ° C. The method of claim 3 wherein the difference between the cloud point and the pour point of the fuel is greater than about 15 ° C. The method of claim 3 wherein the cetane number of the fuel is greater than about 65. The method of claim 5, wherein the cetane number of the fuel is greater than about 65. The method of claim 3, wherein the fuel is formulated to comprise a 95% point as measured by ASTM D-2887 in excess of 343 ° C. The method of claim 3, wherein the fuel is formulated so as to comprise a 95% point as measured by ASTM D-2887 in excess of 366 ° C. The method of claim 3, wherein the cloud point of the fuel is less than about 0 ° C. The method of claim 3, wherein the cloud point of the fuel is less than about -15 ° C. The method of claim 3 wherein the cloud point of the fuel is less than about -25 ° C. The method of claim 3, wherein the fl surface point depressor comprises a linear component and a branched component. NyaPatentkrav070327 10 15 529 270 22 P1101287SE00 The method of claim 13, wherein the branched chain component is selected from the group consisting of fumarates, bridged alkyl aromatics, acrylates, and acetates. The method of claim 3, the diesel fuel is greater than about 10 mg / kg. wherein the amount of pour point depressor in The method of claim 3 wherein the amount of pour point depressant in the diesel fuel is greater than about 50 mg / kg and less than about 1000 mg / kg. The method of claim 3, the diesel fuel being greater than about 100 mg / kg and less than about 500 mg / kg. The method of claim 3, wherein the paraffin wax content of the fuel is substantially wherein the amount of fl surface point depressant in solution. The method of claim 3, wherein the temperature of the fuel is above the cloud point of the fuel. The method of claim 3, wherein the fuel has a sulfur content of less than about 1 ppm and an aromatic content of less than about 1% by weight. NyaPatentkrav070327